Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/02—Elements
  • C08K3/08—Metals
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
  • C09K15/00—Anti-oxidant compositions; Compositions inhibiting chemical change
  • C09K15/02—Anti-oxidant compositions; Compositions inhibiting chemical change containing inorganic compounds
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
  • B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
  • B22F1/16—Metallic particles coated with a non-metal
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function

Definitions

• the present invention relates to an oxygen- absorbing composition for combining with a resin to impart an oxygen-absorbing quality thereto so that it can be used as plastic packaging material for the purpose of absorbing oxygen within a container which includes such packaging material.
• various resins are used as containers for various foodstuffs and materials which may be deleteriously affected by oxygen. It is desirable to have an oxygen- absorber as a component of the packaging material so that any oxygen within the container can be absorbed thereby. Furthermore, it is desirable that the oxygen-absorber should be one which acts reasonably rapidly in the packaging material so that it will absorb the oxygen before the oxygen can materially affect the quality of the goods, such as food, within the container. It is with such an oxygen absorbing composition for use as a component of a resin packaging material that the present invention is concerned.
• Another object of the present invention is to provide an improved oxygen-absorbing composition for use as a component of resin packaging material which is relatively simple and which will combine well with a plastic.
• a further object of the present invention is to provide an improved oxygen-absorbing composition for use as a component of resin packaging material which will not detract from the physical characteristics of a container or package.
• the present invention relates to an oxygen- absorbing composition for combination with a resin to effect oxygen-absorption thereby comprising in relatively sufficient proportions iron, an acidifier and an electrolyte.
• the present invention also relates to an oxygen-absorbing composition for combination with a resin to effect oxygen-absorption thereby consisting essentially in relatively sufficient proportions iron, an acidifier and an electrolyte .
• the oxygen-absorbing composition of the present invention is for use as a component of resin packaging materials, including rigid plastic containers and flexible packaging materials, including sheet and film plastics.
• the oxygen-absorbing composition of the present invention comprises in relatively sufficient proportions iron, an acidifier, which is preferably sodium bisulfate, and an electrolyte, which is preferably sodium chloride.
• an acidifier which is preferably sodium bisulfate
• an electrolyte which is preferably sodium chloride.
• the iron in the presence of an electrolyte functions as an oxygen- absorber.
• the acidifier in the composition provides an acidic environment which hastens the oxygen-absorption.
• an oxygen-absorbing composition including iron, acidifier and the electrolyte was previously used as a component of a resin to cause the resin to have desirable oxygen-absorbing qualities.
• the types of iron which can be used are hydrogen reduced iron, especially sponge grade, annealed electrolytically reduced iron and carbonyl iron.
• the hydrogen reduced sponge grade iron is preferred because it has been found that it functions significantly better than other irons. It is believed that this better functioning is due to the fact that the sponge grade hydrogen reduced iron has a rough surface which is larger than the surface of annealed electrolytically reduced iron which is spherical.
• other types of iron including but not limited to non-annealed electrolytically reduced iron can also be used in addition to the various irons noted above.
• the iron may be present by weight in an amount of between about 50% and 98%, and more preferably between about 75% and 95%, and most preferably between about 80% and 90%.
• the majority of the iron may have a size of between about 150 microns and 1 micron, and more preferably between about 100 microns and 5 microns, and most preferably between about 50 microns and 5 microns.
• the sodium bisulfate may be present by weight in an amount of between about 1% and 30%, and more preferably between about 4% and 20%, and most preferably between about 5% and 18%.
• the majority of the sodium bisulfate may have a size of between about 150 microns and 1 micron, and more preferably between about 100 microns and 5 microns, and most preferably between about 50 microns and 5 microns.
• the sodium bisulfate or any other acidifier may be applied as a solution to the iron and the solvent can then be removed, leaving a deposit of the acidifier on the iron.
• the sodium chloride which is the preferred electrolyte, may be present by weight in an amount of at least about .1% provided that it is mixed well enough with the other components to produce the desired electrolytic action, and more preferably between about .5% and 4%, and most preferably between about 1% and 3%.
• any excess salt merely takes the place of iron which actually produces the oxygen-absorption.
• the majority of the sodium chloride may have a particle size of between about 150 microns and 1 micron, and more preferably between about 100 microns and 5 microns, and most preferably between about 50 microns and
• the sodium chloride or any other electrolyte may be applied as a solution to the iron and the solvent can then be removed, leaving a deposit of the electrolyte on the iron.
• the electrolyte and the acidifier may be carried by the same solvent and applied to the iron simultaneously.
• sodium chloride is the preferred electrolyte
• other electrolytes including but not limited to potassium chloride, sodium iodide and calcium chloride may be of the same size ranges and be used in the same proportions as noted above for the sodium chloride .
• compositions which were found to function satisfactorily when combined with polyethylene and with poly-ethylene-terephthalate comprised by weight (1) 80% iron, 16% sodium bisulfate and 4% sodium chloride, and (2) 90% iron, 8% sodium bisulfate and 2% sodium chloride.
• the preferred composition consisted by weight of 90% hydrogen reduced sponge grade iron, 8% sodium bisulfate and 2% sodium chloride.
• the iron was of a particle size which passed through a 325 mesh screen having the designation W USA Standard Sieve ASTM Specification E-ll.”
• the particle size analysis of the foregoing iron was: 11.8% was less than 10 microns, 27.03% was above 36 microns and the average was 28.25 microns.
• the distribution of particle sizes will vary from batch to batch.
• Annealed electrolytically reduced iron was also found to be satisfactory in the above composition.
• the sodium bisulfate was ground to a size which passed through a 325 mesh screen.
• the sodium bisulfate had an average size of eight microns with a top size of 20 microns.
• the sodium chloride was a commercially obtainable 325 mesh size, and the particle size distribution was 1% was greater than 200 mesh (74 microns) , 95% was less than 325 mesh (43 microns) .
• EXAMPLE I Pelletized Dowlex 2517 linear low density polyethylene was melted in an oven. Once melted, 2.5% by weight of the following oxygen-absorbing blend was thoroughly mixed in.
• the oxygen-absorbing blend consisted by weight of 90% sponge grade hydrogen reduced iron which passed through a 325 mesh screen and had a size distribution wherein 11.8% was less than 10 microns, 27.03% was above 36 microns and the average was 28.25 microns.
• the oxygen-absorbing blend also contained 8% by weight of sodium bisulfate and 2% by weight of sodium chloride, both of which had the size ranges set forth in the preceding paragraph. Prior to mixing the oxygen- absorbing composition with the melted polyethylene, it was blended in a Hobart mixer. The oxygen-absorbing blend was not milled after blending.
• a three- inch by three-inch piece of wet blotter paper was also placed in the pouch as a moisture source to provide moisture for the oxygen-absorbing reaction.
• the pouch was then vacuum sealed.
• the pouch was then filled with 500 cc of gas containing .4% oxygen and 99.6% nitrogen through a septum on the pouch. Since it was not possible to vacuum all of the original air out of the pouch, the oxygen content in the pouch was 1.5% as measured by a Mocon Pac Check Model 450 Head Space Analyzer. Initial oxygen readings were taken and then readings were taken every few days to measure the rate of oxygen- bsorption. The oxygen-absorption is set forth in Table I.
• EXAMPLE II This example was performed in the same manner as described above in EXAMPLE I except that the oxygen- absorbing blend was milled in accordance with the following procedure.
• the same composition as described in EXAMPLE I was not blended in a Hobart mixer, but was blended in a Forberg mixer and the iron, sodium bisulfate and sodium chloride were then milled together in a jet mill to further decrease the particle size to an average of 25 microns with a range of 3 to 80 microns.
• the oxygen-absorption is set forth in Table I .
• EXAMPLE III This example was performed in the same manner as described above in EXAMPLE I except that the oxygen-absorbing blend consisted by weight of 80% sponge grade hydrogen reduced iron, 16% sodium bisulfate, and 4% sodium chloride. The oxygen-absorption is set forth in Table I.
• EXAMPLE IV This example was performed in the same manner as described above in EXAMPLE II except that the oxygen-absorbing blend was the same as set forth in EXAMPLE III .
• the oxygen-absorption is set forth in TABLE I.
• EXAMPLES I, II, III and IV The oxygen-absorbing characteristics of EXAMPLES I, II, III and IV are set forth in the following TABLE I along with a column labeled "Iron+ NaCI" which consisted of iron and sodium chloride which were unmilled and blended in a Hobart mixer. The iron and sodium chloride were then combined with molten polyethylene and then a film was made and tested for oxygen-absorbing capability in accordance with the procedure of EXAMPLE I.
• the sodium chloride had a 325 mesh size as described above, and the iron had an average 28 micron size.
• EXAMPLE VI This example was performed in the same manner as EXAMPLE II except that the resin is a polyester as set forth in EXAMPLE V.
• the oxygen-absorbing characteristics are set forth in TABLE II.
• EXAMPLE VII This example was performed in the same manner as EXAMPLE III except that the resin is a polyester as set forth in EXAMPLE V.
• the oxygen-absorbing characteristics are set forth in TABLE II.
• EXAMPLE VIII This example was performed in the same manner as EXAMPLE IV except that the resin is a polyester as set forth in EXAMPLE V.
• EXAMPLES V, VI, VII and VIII are set forth in TABLE II along with a column labeled "Iron+ NaCI” which consisted of iron and sodium chloride which were unmilled and blended in a Hobart mixer. The iron and sodium chloride were then combined with molten polyethylene and then a film was made and tested for oxygen-absorbing capability in accordance with the procedure of EXAMPLE I .
• the sodium chloride had a 325 mesh size as described above, and the iron had an average 28 micron size.
• EXAMPLE IX This example was preformed in the same manner as EXAMPLE II and all parameters were the same except that the original oxygen content in the pouch was different.
• This example had the same formulation as EXAMPLES II and IX except that each of the ingredients of the oxygen-absorbing composition were milled separately and then blended in a Hobart mixer. As noted above, in
• EXAMPLES II and IX in the oxygen-absorbing composition, the ingredients were milled together. After the separate milling the size range of the iron was an average of 22 microns. The size range of the sodium bisulfate was an average of 8 microns . The size range of the sodium chloride was an average of 8 microns .
• EXAMPLES IX and X The oxygen-absorbing characteristics of EXAMPLES IX and X are set forth in the following TABLE III along with a column labeled "Iron+ NaCI" which consisted of iron and sodium chloride which were unmilled and blended in a Hobart mixer. The iron and sodium chloride were then combined with molten polyethylene and then a film was made and tested for oxygen-absorbing capability in accordance with the procedure of EXAMPLE I .
• the sodium chloride had a 325 mesh size as described above, and the iron had an average 28 micron size.
• a selected oxygen-absorbing resin composition of the type such as described in EXAMPLES I-VIII is pelletized and added to the same respective basic resin during the formulation of the ultimate products, such as bottles, sheets, films, trays and containers of various sorts. Therefore the percentage of the oxygen-absorber in the ultimate product will be a much lower percentage than shown in the above examples.
• the above specifically described resin compositions of EXAMPLES I-VIII may be used at full strength to produce the final product .
• the oxygen-absorbing composition will also work with medium density and high density polyethylene and in varying degrees with other resins including but not limited to polypropylene, nylon, polyvinyl alcohol, urethane, acrylic, polyvinyl chloride and polystyrene, and various blends and copolymers thereof, depending on their specific permeabilities.

Landscapes

• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Inorganic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Materials Engineering (AREA)
• Gas Separation By Absorption (AREA)
• Solid-Sorbent Or Filter-Aiding Compositions (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Food Preservation Except Freezing, Refrigeration, And Drying (AREA)

Priority Applications (9)

Applications Claiming Priority (2)

Publications (1)

Family

ID=32297429

Family Applications (1)

Country Status (12)

Families Citing this family (39)

Citations (4)

Family Cites Families (24)

• 2002
  • 2002-11-18 US US10/298,369 patent/US6899822B2/en not_active Expired - Lifetime
• 2003
  • 2003-10-14 MX MXPA05005029A patent/MXPA05005029A/es active IP Right Grant
  • 2003-10-14 KR KR1020117001745A patent/KR20110011757A/ko not_active Application Discontinuation
  • 2003-10-14 CN CN2008100030340A patent/CN101250286B/zh not_active Expired - Fee Related
  • 2003-10-14 CN CNB2003801068961A patent/CN100371412C/zh not_active Expired - Fee Related
  • 2003-10-14 AU AU2003285873A patent/AU2003285873B2/en not_active Ceased
  • 2003-10-14 ES ES03779100T patent/ES2390340T3/es not_active Expired - Lifetime
  • 2003-10-14 JP JP2004553442A patent/JP4249707B2/ja not_active Expired - Lifetime
  • 2003-10-14 EP EP03779100A patent/EP1570020B1/en not_active Expired - Lifetime
  • 2003-10-14 KR KR1020057008984A patent/KR101056598B1/ko not_active IP Right Cessation
  • 2003-10-14 BR BRPI0316325-3A patent/BR0316325B1/pt not_active IP Right Cessation
  • 2003-10-14 CA CA2506283A patent/CA2506283C/en not_active Expired - Fee Related
  • 2003-10-14 WO PCT/US2003/032634 patent/WO2004046270A1/en active Application Filing
• 2005
  • 2005-05-23 US US11/135,183 patent/US8221647B2/en not_active Expired - Fee Related
• 2008
  • 2008-12-22 HK HK08113866.6A patent/HK1120062A1/xx not_active IP Right Cessation
• 2009
  • 2009-04-24 AU AU2009201631A patent/AU2009201631B2/en not_active Ceased

Patent Citations (4)

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events